More on Vapor Cloud Explosions and Fires
Dr. John Nordin
The Chemical
Safety Board, which is the federal organization that investigates chemical
accidents at facilities in the United States, has recently identified two types
of accidents that are occurring somewhat frequently resulting in death. That
organization is recommending changes in industry standards and also regulations
to minimize accidents, but first responders also need to recognize the
situations. Both kinds of accidents involve natural gas or hydrocarbon
vapors which contact an ignition source resulting in explosion and fire. One
class of accident occurs when industry or power companies purge and vent lines
or equipment with natural gas before placing into service. The other accident
occurs when unauthorized people (usually teenagers) hangout at unsecured oil
and gas production sites.
Kleen Energy Natural Gas Explosion,
Middletown CT, Six Workers Killed.
On 7
February 2010 (Sunday), Kleen Energy at Middletown, Connecticut, experienced a
catastrophic natural gas explosion which caused six deaths, at least 50
injuries, and significant damage to the billion dollar facility. The U.S.
Chemical Safety and Hazard Investigation Board (“Chemical Safety Board”)
findings on this accident is available through links at their website,
http://www.csb.gov/.
The explosion
occurred at Kleen Engergy’s combined-cycle natural gas fueled power plant which
was finishing the final stages of construction and beginning startup. By
“combined cycle” is meant that natural gas is combusted to drive massive
turbines with the residual heat from combustion used to generate steam, which
in turn is used to drive more turbines as in a conventional power plant. It is
essential that the flue gas (from combustion of natural gas) used to drive the
turbines be clean, that is, free of anything that might deposit on the turbine
blades. This means that the lines used to convey the natural gas and flue gas
must be absolutely free of any debris resulting from construction. There must
be pipe cleaning before startup. Kleen Energy used the natural gas available
at the site at 650 pounds per square inch pressure to purge their lines venting
the gas to the outside air. A total of 15 natural gas blows were completed
intermittently over a four-hour period on February 7 prior to the explosion
which occurred at approximately 10:15 AM. According to Chemical Safety Board
calculations, a little over 2 million standard cubic feet of natural gas were
used for purging in the morning with about 400,000 standard cubic feet released
10 minutes prior to the incident. Venting occurred at several outdoor open
pipe locations located less than 20 feet off the ground including one as such
as shown in figure 1.
The Chemical
Safety Board (CSB) investigation (
http://www.csb.gov/investigations/detail.aspx?SID=91&Type=2&pg=1&) noted that while Kleen Energy
followed written procedures for venting and also took care to remove outdoor
ignition sources, work continued inside the main power generation building
including welders actively working. The building electric power was on, and
diesel-fueled heaters were running. OSHA investigation also noted that
several of the 150 workers on site on the day of the explosion had worked in excess
of 90 hours during the previous week. Some workers inside the building made a
personal decision to exit the building prior to the explosion because they were
alarmed by the smell of the natural gas odorant. All six fatalities and 50+
injuries were within the building. As seen by Figure 1, the natural gas
venting may occur in somewhat confined spaces near building structures. The
vents were adjacent to the south wall of the building.
The exact
ignition source at Kleen Energy was never determined. CSB said that the gas
blow itself can be self-igniting, from static electricity or from expelled
metal debris sparking against nearby structures. The Lower Explosive Limit for
natural gas is 4% natural gas in air.
Figure 1: Natural gas venting during
purging of lines, photo taken on Feb. 7 before explosion (used in CSB report)
Figure 2.
Damaged facility after explosion
Explosion and Fire at Calpine
Wolfskill Power Plant, Fairfield California, 26 January 2003
This
incident occurred on 26 January 2003 during pre-commissioning of the Wolfskill
Energy Center natural gas power plant in Fairfield, California. High-pressure
natural gas at approximately 630 psig was used to flush out the gas lines of
debris and vented through four-inch open-ended pipe directly to the atmosphere.
Seven people were at the site, either directing the operations or observing as
in the case of the local fire department. Non-essential personnel were cleared
from the area. Fortunately no one was injured when the explosion occurred,
which shattered windows a quarter of a mile away and was heard up to ten miles
from the site. The debris was projected over the heads of the people at the
site and did not hit anyone. The ignition source was not determined, but
Calpine’s investigation concluded that the explosion was most likely ignited by
static electricity. Calpine concluded that the use of natural gas to purge
piping while convenient has risks. Calpine facilities now do not allow the use
of natural gas to clean piping and instead use compressed air.
Figure 3. Calpine Wolfskill Power
Plant, 26 January 2003. Photo from CSB report at
http://76.227.217.14/UserFiles/file/FINAL%20Urgent%20Recommendation.pdf.
Figure 4. A gas blow from an
electric power plant used to remove debris from piping. The brown cloud
represents debris in the lines. Photo, Kleen Energy, 30 January 2010, as used
in a CSB report urging changes in regulations and standards,
http://76.227.217.14/UserFiles/file/FINAL%20Urgent%20Recommendation.pdf.
The Chemical
Safety Board conducted a survey of combined cycle natural gas fueled power
plants. Of the 62 responses received, 63% indicated use of “natural gas blows”
to clean piping. One response indicated use of flare to destroy flammables
vented during natural gas blows. Other facilities used pigging and air flow,
air blow, nitrogen blow, chemical and water cleaning, or steam blow or a
combination thereof. The organization also concluded that in the case of
Kleen Energy significantly more gas was released than was actually needed to
clean the piping. They also recommended revising the National Fire Protection
Codes 54, 37, and 850, the ASME B31.1 standard, and FM Global’s “Natural Gas
and Gas Piping” standard to incorporate safer practices. OSHA regulations
contain many gaps in release of flammable gas in the vicinity of workers.
There are no standards specific to the power industry that address the cleaning
of power plant fuel lines. There are safer methods of cleaning fuel lines.
Details are at
http://www.csb.gov/assets/document/Kleen%20Energy%20Public%20Meeting%20Presentation_6%2028%2010.pdf.
Accidents
to Young People Hanging Out at Unsecured Oil/Gas Production Sites
The Chemical
Safety Board has identified 26 accidents and 44 fatalities among teenagers and
young adults hanging out at unsecured oil and gas production during the period
1983 and 2010, of which 16 deaths occurred since 2003. These deaths were not
workers but involved the public less than 25 years of age having access to
tanks containing flammable gases and liquids and unaware of the hazards Many
of the deaths occurred when the victims apparently brought a cigarette, match,
or lighter in contact with vapor from storage tanks. Some recent examples
follow:
·
14 April 2010, 9 PM, near Weeletka, Oklahoma. Six young adults
driving on a public road noticed an open gate and entered an unmanned oil
production site containing four petroleum storage tanks and two brine tanks.
The explosion occurred about 10 minutes after the young adults arrived at a
site, when a 21-year-old male climbed up the catwalk leading to the top of one
of the tanks and opened a hatch and peered inside. The resulting explosion,
apparently caused by a lit cigarette or lighter, killed the man. A second
explosion occurred in an interconnected tank. Another youth suffered second
degree burns. The resulting fire burned for more than three hours before it
was extinguished by several responding fire departments using foam. Figure 5,
below, shows the tanks after fire departments extinguished the fire.
Figure 5. Oil
production site, after fire, from
http://www.csb.gov/newsroom/detail.aspx?nid=315.
CSB investigators spent 4 days at the site interviewing witnesses and
determining what happened. The victim who was killed lived for a few hours
after being engulfed in flames, and was able to describe the accident to
emergency response personnel. The site entrance was protected only by an
unmarked gate which was described as being wide open on the night of April 14,
and generally open and unlocked at other times, and there was no protective fencing.
The tank hatches had no mechanism to allow securement, and the catwalk
leading to the tank top was readily accessible. The CSB investigators also
observed other oil and gas production sites in the area and found most of them
were unsecured and had no warning signs. Oklahoma has approximately 257,000
active and unplugged oil and gas production sites, and requires fencing and
warning signs only at sites that have hydrogen sulfide hazards.
·
31 October 2009, 4 AM, Carnes, Mississippi. Two teenagers (16
and 18 year old) were killed while at an unsecured and unattended oil
production site when a gas condensate tank exploded. The blast hurled the
20-foot-tall tank 60 yards killing the teens. According to the Mississippi Oil
and Gas Board, the explosion likely occurred when the two victims were above
the tank which was accessible by a catwalk. The tank contained approximately
14 barrels of oil and had a flammable atmosphere. The site did not have
fences, barriers, or warning signs. The oil tank was located near the home of
one of the two boys who were killed. The CSB investigating the accident could
not determine the ignition source of this incident as there were no surviving
eyewitnesses, but teenagers interviewed after the accident said that it was
common practice for young people to hang out and socialize at oil production
sites. “When we go hang out at an oil site, a bunch of friends and I would
usually get a pack of cigarettes and talk about what’s been going on during the
week. It’s like our own little sanctuary where we can just be away from
everybody”, said one of the teens interviewed and was featured in an 11-minute
CSB safety video titled “No Place to Hang Out: The Danger of Oil Sites”. This
video (figure 6), which was put together by CSB following the Mississippi
deaths is available at
http://www.safetyvideos.gov/newsroom/detail.aspx?nid=313&SID=0&pg=1&.
Figure 6. CSB safety
video, produced after the deaths of two Mississippi teenagers
·
26 April 2010, explosion at about 1:30 AM, near New London , Texas,
County Road 111 in Rusk County. Following an explosion, firefighters arriving
at the scene found the body of a 24-year-old woman and a badly injured
24-year-old man about 150 to 180 feet from a group of oil well tank batteries
at the explosion site. The ignition source for the explosion was not
conclusively determined, but it was believed to be a cigarette lighter that ignited
fumes venting above the tank batteries, and the couple had climbed on top of
the tank and lit a cigarette. The tank that exploded was mostly empty.
Details and photos are available at KLTV, New London,
http://www.kltv.com/Global/story.asp?S=12374145.
The example
accidents reveal a similar pattern. Unauthorized people enter an unsecured oil
production site usually at night. Unaware of hazards, an ignition source,
usually a cigarette or lighter or match contacts flammable vapors resulting in
a vapor cloud explosion and fire. With support from some of the families of
young people killed, the Chemical Safety Board is advocating legislation that
oil and gas production facilities be secured to prevent unauthorized access.
Lessons Learned and Relevance to PEAC
Tool
Both examples describe situations
where a flammable vapor or gas concentration exceeded the lower explosive limit
concentration. The flammable vapor or gas ignited when it contacted an
ignition source. This is basic knowledge for anyone who has to deal with
hazardous materials. The PEAC tool organizes information in one package
necessary to make correct decisions, for example, flammability and lower and
upper explosive limits, and safe distances for “worst case” blast in case of a
vapor cloud explosion. Other informational packages are available and can be
used, but the PEAC tool organizes the information in one package and is easy to
use under stressful situations encountered by first responders.
The examples given here demonstrate a
key missing ingredient. People responsible for making decisions must
recognize potentially hazardous situations and not allow distractions to get in
the way. This knowledge comes with experience. Kleen Energy recognized that
that the lower explosive limit for natural gas was 4% by volume in air and excluded
personnel entry at outdoor locations where natural gas venting took place, but
was also under pressure to bring the new power plant on line. Some of the vent
lines (figure 1) were in confined areas near the power generation building
where about 150 workers were assigned to other projects necessary to bring the
power plant on line, and the workers were not told of the outdoor flushing
activities. Furthermore, not wanting to risk a later shutdown because of
deposits on turbine blades, Kleen Energy flushed much more natural gas through
the lines than what was necessary, according to the Chemical Safety Board.
Also, inherently safer gases (nitrogen, steam flush, etc.) could have been used
for flushing when the facility was being designed. The Chemical Safety Board
also found codes and standards deficient in addressing the problem of
performing line flushes.
In the case of the Wolfskill Power
Plant incident, decision makers recognized the hazards and only allowed
essential personnel to be on site. But venting occurred in a somewhat
confined area allowing explosive mixtures of air and natural gas to build up.
The ignition source was apparently a spark generated due to line debris
striking a metal surface.
Companies may provide oil and gas
production workers information on hazards of flammable gases, liquids, and
vapors, and prohibit smoking. But sites also need to be secure against
unauthorized access by the public. As a minimum, vent ports or covers on tanks
and tank catwalks should be secure and warning signs displayed. The Chemical
Safety Board reviewing codes and standards found a mix of “no standards or
instructions” to varying degrees of specifications for securing a site
depending upon the location. Some California locations require fencing around
the production facility with bobbed wire at the top to make it difficult to
gain access by climbing over the fence. The tendency of oil and gas production
facilities is to comply with local codes and standards if they are aware of
them but do no more.
Many facets must be brought together
in the decision process for recognizing hazardous situations.